(62a) Setting Biorefinery Manufacturing Fundamentals to Produce a Portfolio of Commodity and Fine Chemicals | AIChE

(62a) Setting Biorefinery Manufacturing Fundamentals to Produce a Portfolio of Commodity and Fine Chemicals

Authors 

Inui, M. - Presenter, Research Institute of Innovative Technology for the Earth (RITE)
Vertès, A. A. - Presenter, Research Institute of Innovative Technology for the Earth (RITE)


 The chemurgy concept, that is, manufacturing industrial commodity and chemical products from organic raw materials such as agricultural biomass and lignocellulosic waste, predates the petrochemical industry. However, petrochemicals prevailed over fermentation chemicals given critical industrialization factors, comprising a low cost of the petroleum feedstock and a high process economic efficiency, as exemplified by the full utilization of products and by-products from petrochemical plants for the production of gasoline. These economies of scale and scope have played an important role in the booming industrial development at the beginning of the XXth century and were realized on a very large scale in World War II and the following decades1.

 These extremely efficient cost structures that have been derived in the petrochemical industry over a century are now both a blessing and a curse. The blessing is that these economies of scale and scope have made possible the manufacturing of cheap fuels and materials. The resulting abundant supply of chemicals for industry and transportation has enabled modern life and thus now appear to be indispensable. The curse is that efforts to displace and replace the petroleum industry by the chemurgy industry for alleviating global warming and fossil fuel supply threats meet a very high economic and resistance barrier2. This has resulted over the years in a detrimental delay in renewable chemistry technology investment, development, and deployment3.

 The biorefinery concept aims at recreating for agricultural feedstock cost structures that are similarly enabling as the ones at play in the petrochemical industry4, 5. This change is of course fundamental and will have far reaching consequences, as it integrates the agricultural value chain into the petrochemical value chain, thus colliding the transportation, polymer, and chemical value chains with other established value chains and notably of the food and feed industry3. A key difference nevertheless remains in that the higher oxygen content of biomass-based compounds makes possible to produce totally novel materials and chemicals with novels properties6. An enabling factor of the biorefinery vision is of course the availability of versatile, cost-effective, and robust industrial processes to manufacture an array of chemicals to serve various sectors including the fuel, chemical, industrial polymer, feed, food, cosmetic, and pharmaceutical industries. Notably, it is important for the biorefinery plant manager to be able to produce in addition to fuels, such as ethanol or isobutanol, higher value compounds for the chemical industry, such as ethyl-acetate or isobutanol.

 We report here on a growth-arrested biotechnological process to manufacture ethanol, organic acids, and amino acids from mixed sugars, based on Corynebacterium glutamicum, an organism that has a long history of use to produce amino acids as feed and food supplements or cosmetic ingredients. The intrinsic design of the process is to decouple in a separate fermentor and a reactor biological catalyst-production and product-production phases7 with cell recycling and using very high cell concentrations; it builds upon the intrinsic properties of this organism. C. glutamicum is a facultative anaerobic bacterium that grows in the absence of oxygen only in media containing a terminal electron acceptor such as nitrate8. C. glutamicum does not sporulate but remains metabolically active when placed under growth-arrested conditions9, 10 and is not inhibited by common fermentation inhibitors present in typical lignocellulosic hydrolysates11, 12; moreover, it can catabolize a range of sugars in parallel with glucose7, 13, 14. A complete toolbox of molecular tools enables one to modulate at will its plastic genome and general metabolism10, 15. The RITE process presents the entire set of fundamental attributes necessary for reaching cost-effectiveness and enabling a rich product portfolio: simplicity, industrial robustness16, raw material versatility (glucose, fructose, glucuronic acid, glucosamine, maltose, mannose, α-methyl-glucoside, ribose, sucrose, trehalose, arbutin, salicin, cellobiose, arabinose, xylose)13, 14, 17, 18, product versatility (ethanol, organic acids, amino acids)9, 16, 19, 20, reduced utilities requirement (reduced fermentation heat12, no oxygenation requirement9), high conversion rates of carbohydrate feedstocks-to-product given cell recycling and the absence of growth requirements (e.g., 110 gl-1 or 40 gl-1h-1 D-lactate)21, possibility to conduct continuous fermentations for long periods of time, dramatically reduced risks of contamination in the reaction vessel given the use of very high cellular concentrations, secreted product, no expensive reagent, portfolio of processes that enable the practitioner to manage the biorefinery plant in swiftly interchangeable processes or to capture synergies by implementing multiplex productions22.

 The stage is now set for this core technology to be translated into a biorefinery demonstration plant, as a first step towards full-scale commercialization.

References
1. Benninga, H. A history of lactic acid making. (Kluwer Academic Publishers, Dordrecht, The Netherlands; 1990).
2. Vertès, A.A., Inui, M. & Yukawa, H. Implementing biofuels on a global scale. Nat Biotechnol 24, 761-764 (2006).
3. Vertès, A.A., Qureshi, N., Blaschek, H.P. & Yukawa, H. (eds.) Biomass to biofuels: strategies for global industries. (Wiley, Chichester, UK; 2010).
4. Cherubini, F. The biorefinery concept: using biomass instead of oil for producing energy and chemicals. Energy Conversion Manag 51, 1412-1421 (2010).
5. Octave, S. & Thomas, D. Biorefinery: toward an industrial metabolism. Biochimie 91, 659-664 (2009).
6. Marquardt, W. et al. The biorenewables opportunity: toward next generation process and product systems. AIChE J 56, 2228-2235 (2010).
7. Vertès, A.A., Inui, M. & Yukawa, H. in 14th European Biomass Conference 1068-1071, Paris, France; 2005).
8. Nishimura, T., Vertès, A.A., Shinoda, Y., Inui, M. & Yukawa, H. Anaerobic growth of Corynebacterium glutamicum using nitrate as a terminal electron acceptor. Appl Microbiol Biotechnol 75, 889-897 (2007).
9. Inui, M., Kawaguchi, H., Murakami, S., Vertès, A.A. & Yukawa, H. Metabolic engineering of Corynebacterium glutamicum for fuel ethanol production under oxygen-deprivation conditions. J Mol Microbiol Biotechnol 8, 243-254 (2004).
10. Yukawa, H., Inui, M. & Vertès, A.A. in Amino acid biosynthesis, Vol. 5. (ed. V.F. Wendisch) (Springer Verlag, Berlin, Germany; 2006).
11. Sakai, S. et al. Effect of lignocellulose-derived inhibitors on growth of and ethanol production by growth-arrested Corynebacterium glutamicum R. Appl Environ Microbiol 73, 2349-2353 (2007).
12. Inui, M. et al. in 28th Symposium on Biotechnology for Fuels and Chemicals, Nashville, TN, USA; 2006).
13. Kawaguchi, H., Sasaki, M., Vertes, A.A., Inui, M. & Yukawa, H. Engineering of an L-arabinose metabolic pathway in Corynebacterium glutamicum. Appl Microbiol Biotechnol 77, 1053-1062 (2008).
14. Sasaki, M., Jojima, T., Inui, M. & Yukawa, H. Simultaneous utilization of D-cellobiose, D-glucose, and D-xylose by recombinant Corynebacterium glutamicum under oxygen-deprived conditions. Appl Microbiol Biotechnol 81, 691-699 (2008).
15. Vertès, A.A., Inui, M. & Yukawa, H. Manipulating corynebacteria, from individual genes to chromosomes. Appl Environ Microbiol 71, 7633-7642 (2005).
16. Vertès, A.A., Inui, M. & Yukawa, H. Technological options for  biolofical fuel ethanol. J Mol Microbiol Biotechnol 15, 16-30 (2008).
17. Yukawa, H. et al. Comparative analysis of the Corynebacterium glutamicum group and complete genome sequence of strain R. Microbiology 153, 1042-1058 (2007).
18. Kawaguchi, H., Vertès, A.A., Okino, S., Inui, M. & Yukawa, H. Engineering of a xylose metabolic pathway in Corynebacterium glutamicum. Appl Environ Microbiol 72, 3418-3428 (2006).
19. Inui, M. et al. Metabolic analysis of Corynebacterium glutamicum during lactate and succinate productions under oxygen deprivation conditions. J Mol Microbiol Biotechnol 7, 182-196 (2004).
20. Okino, S. et al. An efficient succinic acid production process in a metabolically engineered Corynebacterium glutamicum strain. Appl Microbiol Biotechnol 81, 459-464 (2008).
21. Okino, S., Suda, M., Fujikura, K., Inui, M. & Yukawa, H. Production of D-lactic acid by Corynebacterium glutamicum under oxygen deprivation. Appl Microbiol Biotechnol 78, 449-454 (2008).
22. Vertès, A.A., Inui, M. & Yukawa, H. Alternative technologies for biotechnological fuel ethanol manufacturing. J Chem Technol Biotechnol 82, 693-697 (2007).